Classifications

• • C—CHEMISTRY; METALLURGY
  • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
  • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
  • C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
  • C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
  • C04B35/626—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
  • C04B35/63—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B using additives specially adapted for forming the products, e.g.. binder binders
  • C04B35/632—Organic additives
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
  • B22F3/00—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
  • B22F3/22—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces for producing castings from a slip
• • C—CHEMISTRY; METALLURGY
  • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
  • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
  • C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
  • C04B35/01—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
  • C04B35/26—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on ferrites
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01F—MAGNETS; INDUCTANCES; TRANSFORMERS; SELECTION OF MATERIALS FOR THEIR MAGNETIC PROPERTIES
  • H01F41/00—Apparatus or processes specially adapted for manufacturing or assembling magnets, inductances or transformers; Apparatus or processes specially adapted for manufacturing materials characterised by their magnetic properties
  • H01F41/02—Apparatus or processes specially adapted for manufacturing or assembling magnets, inductances or transformers; Apparatus or processes specially adapted for manufacturing materials characterised by their magnetic properties for manufacturing cores, coils, or magnets

Definitions

• DE-Cl-40 33 952 proposes a binary binder system of the type of sol-d polymer solutions for the processing of metal powder by injection molding. The production of magnets by this method is not mentioned.
• the binary binder system consists of polyethylene and / or polypropylene as the polymeric binder component and cyclododecane, cyclododecanone, cyclododecanol and / or stearyl alcohol as the low molecular weight binder component.
• EP-A-0 115 104 describes a process for the production of sintered inorganic moldings, which is likewise not aimed at the production of magnets.
• carbides, nitrides, borides and sulfides are mentioned as starting materials.
• the moldings are produced by injection molding or extrusion.
• An essential feature of the process is the use of a mixture of an oxidized wax and stearic acid as a plasticizer and binder.
• the agglutinable particles which are generally used as aqueous dispersions, are pressed into a green body in a magnetic field. The particles are then in the anisotropic orientation, which is for the later magnetization of the sintered shaped bodies is advantageous. After pressing, the particles are first demagnetized again, because magnetized green bodies without plasticizers and binders are mechanically extremely sensitive. Because of this sensitivity, the demagnetization of the green bodies must still take place in the form.
• green bodies which are produced by another bt-named process, namely with the addition of organic plasticizers and binders by shaping with magnetic orientation, are mechanically sufficiently stable for further processing and are therefore also good before sintering manageable.
• they are demagnetized before sintering.
• the organic plasticizers and binders must be removed from the green body before sintering. If this is not done with sufficient care, the green body will disintegrate as a result of the evolution of gas and the particles will not later sinter.
• “Debinding" is a critical manufacturing step that should be kept as short as possible for economic reasons.
• the grains produced using organic plasticizers and binders are more prone to cracking during sintering than the wet-pressed ones.
• the method according to claims 1 to 6 is avoided the disadvantages of the prior art described. It is particularly suitable for the production of magnets, in particular segment magnets, as are used in electric motors.
• the green bodies can be produced by injection molding, extrusion or pressing, expediently in an orienting magnetic field.
• the extrusion enables an endless processing of the hard ferrites. For example, segment magnets with an overlap angle of> 140 ° can be easily produced.
• the green bodies, regardless of which of the above-mentioned deformation processes are manufactured, are mechanically sufficiently stable for all further manufacturing steps.
• the plasticizers and binders according to the invention can be removed from the green bodies more quickly and more gently than the plasticizers and binders according to the prior art.
• the green bodies do not hinder the alignment of the ferrite particles in the magnetic field during the production of the green bodies, and the orientation once impressed remains even when "baking” or "debinding", ie the removal of the binding and plasticizing agents by heating , receive.
• the green bodies are characterized by high dimensional stability. Therefore, the shaped bodies generally do not have to be reworked after sintering. This applies particularly to molded articles produced by pressing.
• the moldings produced by the process of the invention also tend to crack to a similar extent as moldings produced by wet pressing. Magnets produced by the process of the invention have good magnetic properties which are not inferior to those of the magnets produced by wet pressing without plasticizers and binders.
• the method according to the invention is particularly suitable for the production of magnets, in particular segment magnets.
• Hard ferrites that can be used for this are, for example, barium ferrite (BaFe 0) and in particular strontium ferrite (SrFe 0).
• Other hard ferrites useful in the manufacture of magnets can also be used.
• the hard ferrites are generally used as powders with average particle sizes in the range from 5 to 20 ⁇ m.
• the powders are produced in the customary manner, for example by milling, for example in vibratory or ball mills, of the mixed oxides obtained by precipitation from aqueous solution and are commercially available.
• stearic acid should act as a dispersant for the hard ferrites.
• the optimal amount of plasticizer and binder depends on the type of hard ferrite used and its average particle size and can be easily determined by means of orienting tests. In general, 0.1 to 30 percent by weight and advantageously 1 to 25 percent by weight of plasticizing agent, based on the weight of the hard ferrite powder, is used.
• the total amount of plasticizer and binder required can be significantly reduced compared to an equally effective amount of only one of the components. This is one of the reasons why, as already mentioned, the removal of the plasticizing and binding agent according to the invention from the green body before the sintering is particularly quick and nevertheless gentle.
• the quantitative ratio of the two components (a) and (b) can vary within wide limits. Generally one works with weight ratios from 9 to 5:95, expediently with a weight ratio of cwa 65:35. If a mixture of two of the substances mentioned or of all three substances is used as component (b), these substances can be present in any mixing ratio, even in those in which the substances do not form single-phase mixtures.
• the hard ferrite powder and the components of the plasticizer and binder are mixed intimately. This can be done in any order, for example by mixing all three substances simultaneously or by adding the other two to one of the three substances in succession.
• the usual devices which exert a sufficient shear effect on the substances to be mixed are suitable for the mixing process, for example a trough kneader, SIGMA kneader, etc. Elevated temperatures, for example from 50 to 150 ° C., promote mixing.
• the mixture obtained is then shaped into green bodies by injection molding, extrusion (extrusion) or advantageously by pressing. This is conveniently done in an orienting magnetic field with a field strength of> 600 kA / m.
• the plasticizer and binder are removed from the green bodies at temperatures which are expediently up to about 650 ° C. and in an oxygen-containing atmosphere, advantageously in air.
• the optimal rate of temperature increase and the duration of the heating depend, among other things. on the layer thickness of the molded body and can in turn be easily determined by orienting tests. It starts at room temperature and the temperature is generally increased by 1 to 100 K / min.
• the plasticizer and binder is generally removed after 10 to 120 hours to such an extent that the green bodies can be sintered.
• the debindered green bodies can be sintered in a manner known per se.
• the debinding and the sintering are expediently drawn together in one operation in the same oven, for example by gradually heating the green bodies to 1200 to 1350 ° C. in an oxygen-containing atmosphere, such as air, and ge at this temperature for 10 to 30 minutes will hold.
• the temperature in the range from 20 ° C to about 600 ° C is expedient with an increase rate of 20 up to 4 'k / min and and in the range from about 600 ° C to the peak temperature, appropriately increased with a rate of increase from 200 to 400 K.
• 850 g of a commercially available strontium ferrite, 100 g cyclodo-decane and 50 g stearic acid are mixed in a kneader for 1 hour at 70 ° C., the mixture is granulated after cooling and comminuted in a cutting mill. The shredded material is pressed into 5 mm thick magnetic segments at 80 ° C. In only one production step, the plasticizing and binding agent is removed and the deboned green bodies are sintered.
• the green bodies are heated in an air-purged electric furnace with a temperature increase rate of 30 K / h from 20 ° C to 600 ° C and with a temperature increase rate of 300 K / h to 1,250 ° C and kept at this temperature for 15 minutes.

Landscapes

• Engineering & Computer Science (AREA)
• Chemical & Material Sciences (AREA)
• Ceramic Engineering (AREA)
• Manufacturing & Machinery (AREA)
• Organic Chemistry (AREA)
• Structural Engineering (AREA)
• Materials Engineering (AREA)
• Inorganic Chemistry (AREA)
• Power Engineering (AREA)
• Mechanical Engineering (AREA)
• Hard Magnetic Materials (AREA)
• Magnetic Ceramics (AREA)
• Press-Shaping Or Shaping Using Conveyers (AREA)
• Manufacturing Cores, Coils, And Magnets (AREA)

Priority Applications (4)

Applications Claiming Priority (2)

Publications (1)

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Family Applications (1)

Country Status (7)

Families Citing this family (12)

Citations (4)

Family Cites Families (10)

• 1994
  • 1994-09-27 DE DE4434471A patent/DE4434471C1/de not_active Expired - Fee Related
• 1995
  • 1995-09-02 EP EP95929741A patent/EP0783466B1/de not_active Expired - Lifetime
  • 1995-09-02 WO PCT/DE1995/001189 patent/WO1996009998A1/de active IP Right Grant
  • 1995-09-02 US US08/765,867 patent/US6063322A/en not_active Expired - Fee Related
  • 1995-09-02 JP JP08511160A patent/JP3099895B2/ja not_active Expired - Fee Related
  • 1995-09-02 KR KR1019970701487A patent/KR100282317B1/ko not_active IP Right Cessation
  • 1995-09-02 ES ES95929741T patent/ES2127547T3/es not_active Expired - Lifetime

Patent Citations (4)

Non-Patent Citations (1)

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